WO2013135684A1 - Procédé de production amélioré de fibrinogène et fibrinogène ainsi produit - Google Patents

Procédé de production amélioré de fibrinogène et fibrinogène ainsi produit Download PDF

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Publication number
WO2013135684A1
WO2013135684A1 PCT/EP2013/054983 EP2013054983W WO2013135684A1 WO 2013135684 A1 WO2013135684 A1 WO 2013135684A1 EP 2013054983 W EP2013054983 W EP 2013054983W WO 2013135684 A1 WO2013135684 A1 WO 2013135684A1
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Prior art keywords
fibrinogen
chelating agent
concentration
glycine
solution
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PCT/EP2013/054983
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English (en)
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Petra Schulz
Werner Gehringer
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Octapharma Ag
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Application filed by Octapharma Ag filed Critical Octapharma Ag
Priority to CN201380013042.2A priority Critical patent/CN104321340B/zh
Priority to RU2014139974A priority patent/RU2663792C2/ru
Priority to US14/382,712 priority patent/US10112972B2/en
Priority to EP13709190.6A priority patent/EP2825555B1/fr
Priority to AU2013231321A priority patent/AU2013231321B2/en
Priority to MX2014010492A priority patent/MX351340B/es
Priority to ES13709190.6T priority patent/ES2642383T3/es
Publication of WO2013135684A1 publication Critical patent/WO2013135684A1/fr
Priority to IL234226A priority patent/IL234226B/en
Priority to US16/136,003 priority patent/US11401300B2/en

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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07K—PEPTIDES
    • C07K14/00—Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof
    • C07K14/435—Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from animals; from humans
    • C07K14/745—Blood coagulation or fibrinolysis factors
    • C07K14/75—Fibrinogen
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07K—PEPTIDES
    • C07K1/00—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
    • C07K1/14—Extraction; Separation; Purification
    • C07K1/36—Extraction; Separation; Purification by a combination of two or more processes of different types

Definitions

  • the present invention relates to a process for purifying fibrinogen from a fibrinogen containing source, a fibrinogen product obtainable according to the process of the invention as well as an anion exchange resin selected from the group con- sisting of a support material comprising a hydroxylated polymer backbone with grafted tertiary or quaternary amino groups for purification or manufacturing of a fibrinogen product.
  • Fibrinogen also known as clotting factor I, plays a key role in haemostasis and wound healing. It is a glycoprotein synthesized in the liver with an apparent molecular weight of 340,000 Da, is composed of two dimers, each of them built of three pairs of non-identical polypeptide chains called ⁇ , ⁇ and ⁇ linked by disulfide bridges. It circulates in the blood stream at a concentration of approximately 1.5 - 4.0 mg/ml. Upon injury of blood vessels, blood platelets are acti- vated and a plug is formed . Fibrinogen is involved in primary haemostasis by aiding cross-linking of activated platelets.
  • fibrinogen is converted into fibrin by proteolytic release of fibrinopeptide A and - at a slower rate - fibrinopeptide B by thrombin.
  • the soluble fibrin monomers are as-flectd to double stranded twisted fibrils. Subsequently these fibrils are arranged in a lateral manner, resulting in thicker fibers. These fibers are then cross-linked by FXIIIa to a fibrin network, which stabilizes the platelet plug by interactions of the fibrin with activated platelets, resulting in a stable clot.
  • Congenital afibrinogenaemia is a rare bleeding disorder, where patients are suffering from inadequate clotting of the blood due to lacking or malfunction of fibrinogen. This medical condition might lead to spontaneous bleeding episodes or excessive bleeding after minor traumata or during interventional procedures.
  • Acquired deficiencies in fibrinogen are much more common than congenital afibrinogenaemia and may be induced by haemodilution or other events such as blood losses during surgery, traumata, disseminated intravascular coagulation (DIC) or sepsis.
  • DIC disseminated intravascular coagulation
  • Fibrinogen deficiencies can be corrected to normal fibrinogen levels in plasma of about 1.5-4 g/l by replacement therapy with intravenous infusion of fresh frozen plasma or cryoprecipitate.
  • these treatments are afflicted with the risk of introduction of pathogens, e.g. viruses or prions, into a patient and are thereby generating additional disorders. It is thus advisable to intravenously apply virus inactivated fibrinogen compositions to restore fibrinogen at physiological levels in a save way.
  • fibrinogen in preparations called fibrin glue, fibrinogen adhesive, tissue glue and similar
  • these preparations are intended for topical use as powders, pastes, foams or in combination with fabrics as plaster on wounds, they are not useable for intravenous application as their consistency and composition would immediately initiate thrombotic events when being injected.
  • These prepa- rations additionally contain thrombin, calcium salts and relatively high amounts of coagulation factor XIII. Examples for such preparations are US-A1-2008/003272, WO-A-95/22316 or US-A1-2008/181878.
  • EP-Al-1 240 200 which relates to a method of purifying fibrinogen from a fibrinogen containing solution, comprising, application of a fibrinogen containing solution to an ion exchange matrix, under conditions such that fibrinogen binds to the matrix, washing the ion exchange matrix with a buffer solution comprising at least one co-amino acid, eluting the fibrinogen from the matrix with a buffer consisting of 10 mM Tris, 10 mM citrate, 45 mM sucrose and NaCI at a concentration of 200 mM to 1.0 M, and optionally recovering the fibrinogen from the eluate.
  • EP-Al-0 771 324 refers to a process for production of a virus free fibrinogen concentrate which is obtained by subjecting a solubilised plasma fraction containing fibrinogen to a chemical viral inactivation treatment, i.e. a S/D or solvent/detergent treatment, subjecting the resulting viral-inactivated fraction to precipitation in a solution containing an amino acid at an acidic pH to obtain a supernatant, filtering the supernatant to obtain a purified fibrinogen concentrate, and recovering the purified fibrinogen concentrate.
  • the recovered fibrinogen concentrate is subjected to ultra violet radiation for a second virus inactivation.
  • the product is stabilized and lyophilized prior to a third virus inactivation step.
  • EP-Al-1 519 944 teaches the use of an immobilized metal ion affinity chroma- tography matrix under conditions that the fibrinogen and plasminogen bind to the matrix, and selectively eluting the fibrinogen and 93% of plasminogen separately from the matrix.
  • EP-Al-0 555 135 discloses a method for production of an intravenously applicable fibrinogen by purification of a fibrinogen solution by means of an anion ex- change gel based on cross-linked agarose comprising quaternary amine groups.
  • the fibrinogen produced is said to be free of factor VIIIc.
  • EP-Al-1 457 497 refers to a process for removing viruses in fibrinogen solutions characterized by stabilization and freezing of the solution and subsequent thawing thereof. Separation of undissolved materials occurs prior to dilution of the protein and is followed by nanofiltration of the resultant solution using filters of a pore size smaller than 35 nm.
  • US-A1-2006/0009376 also discloses a method to manufacture fibrinogen, following repeated dissolution and precipitation of fibrinogen to remove factor XIII.
  • WO-A2-2009/155626 refers to a process for purification of fibrinogen by solubili- sation of cryoprecipitate or Conn-Fraction I in an EDTA-solution at a temperature range of 3°C to 5°C, followed by fractionated precipitation in a temperature range of 2°C to 4°C and dissolution of the last precipitate in an EDTA-solution.
  • Virus inactivation with S/D reagents and nanofiltration for improvement of pathogen safety occur in the presence of EDTA.
  • Inhibition of residual amounts of pro- teases in the produced concentrate is accomplished by addition of AT-III, hepa- rin-cofactor-II and Cl-esterase-inhibitor.
  • US-B2-7,919,592 describes a method for removing viruses from fibrinogen solutions by addition of chaotropic substances, chosen from arginine, guanidine, citrulline and urea, there salts or derivatives and subsequent filtration through nanofilters of various pore size.
  • chaotropic substances chosen from arginine, guanidine, citrulline and urea, there salts or derivatives and subsequent filtration through nanofilters of various pore size.
  • Goheen, S. C. et al . report in Journal of Chromatography A. 816 (1998) 89-96, about HPLC ion-exchange chromatography of the plasma proteins albumin, fibrinogen, and immunoglobulin (G) on nonporous column materials containing either quarternary amine or sulfopropyl functional groups.
  • One object of the invention is providing of a fibrinogen concentrate manufactured with dedicated pathogen eliminating and/or inactivation steps in the production process in order to overcome adverse reactions or development of pathogen related illnesses.
  • Said pathogens are selected from the groups of bacteria, viruses and prions, such as prion protein scrapie (PrP sc ).
  • Nanofiltration is a method in principle known to remove viruses from proteins passing through the nanofilter, but separation of viruses from fibrinogen by nanofiltration is challenging as fibrinogen is a quite large and sticky protein frequently resulting in plugging of filter pores and eventual loss of product.
  • One ap- proach to overcome this problem is to add chaotropic substances to improve fil- terability as it is taught by US-B2-7,919,592, although nanofiltration of a diluted fibrinogen solution produced according to the process of International Application WO-A1-2012/038410 revealed comparable filterability without addition of chaotropic substances.
  • Chaotropic substances according to the invention are those as defined in US-B2-7,919,592 incorporated by reference and designating arginine, guanidine, citrulline and urea, their salts or derivatives.
  • a further object of this application is providing of a process to manufacture a concentrate on an industrial level, i.e. several hundreds to thousands of liters starting material, such as blood or blood plasma, although a small scale produc- tion, i.e. some 1/10 liter to some liters, is also possible.
  • Figure 1 depicts a SDS-Page at non-reducing conditions while figure 2 depicts a SDS-Page at reducing conditions of the same samples.
  • a one-time addition of a rather small amount of at least one chelating agent prior to precipitation, resulting in a total chelating agent concentration of about 3-10 mM, is sufficient for the present invention to provide both excellent yield and filterability, even with nanofilters providing retention of particles of ⁇ 35 nm.
  • Residual amounts of chelating agent can be removed downstream providing a final product, i.e. a fibrinogen concentrate which is free of chelating agent within the detection limit, which is lower than 0.08 pg/rnl for EDTA.
  • a product free of chelating agents is preferable as, for instance, EDTA is a known anti-coagulant.
  • EDTA is a known anti-coagulant.
  • protease inhibitors such as Cl-protease inhibitors, trypsin inhibitors, thrombin inhibitors, antithrombin-III (AT-III), heparin-cofactor-II, aprotinin, pepstatin, leupeptin and in particular epsilon-aminocaproic acid ( ⁇ - ACA) to avoid degradation of fibrinogen is known from prior art literature.
  • the fibrinogen concentrate of the present invention displayed neither a measurable proteolytic activity nor a measurable AT-III concentration.
  • the process of the invention for purification or manufacturing of fibrinogen from fibrinogen containing sources comprises the steps of:
  • the fibrinogen containing source is selected from the group consisting of, blood plasma, plasma fractions, such as fraction I, or cryoprecipitate, cell cultures producing fibrinogen and/or supernatants of said cell cultures. If cryoprecipitate is not used as starting material, a fibrinogen containing intermediate as starting material is produced by well known methods like disclosed by Cohn, Kistler-Nitschmann and modifications thereof.
  • the fibrinogen containing source is subjected to at least one virus inactivating process for example a solvent detergent process as disclosed in EP-Al-0 131 740 incorporated by reference.
  • the virus inactivation is performed prior to forming a fibrinogen enriched precipitate.
  • the removal of virus inactivating substances is performed by oil extraction and/or chromatography with strong anion exchangers.
  • Another method for virus removal is nanofiltration, due to the low content of polymers after fibrinogen extraction nanofiltration can be performed also well with filters ⁇ 35 nm without addition of chaotropic substanc- es.
  • a typical precipitating agent for use in the manufacturing process of the invention is selected from the group consisting of amino acids such as glycine, polyethylene glycol or high salt concentrations, wherein the salt contains monovalent metal ions, in particular selected from the group of alkali metals, or am- monium.
  • the extraction of fibrinogen from the fibrinogen enriched precipitate is performed with a buffer having a pH of 7.5 to 8.5 for 10 to 120 minutes.
  • the stationary phase has ter- tiary or quaternary amino groups.
  • the chromatography steps in the manufacturing process of the invention can in particular be performed in a column.
  • the storage form of the filled fibrinogen enriched fraction is in liquid state, frozen state, preferably at ⁇ -15°C, most preferably below -30°C, or as lyophilisate.
  • step b) virus inactivating the resulting solution of step b) by a solvent/detergent (S/D) treatment, extraction of S/D reagents with vegetable oil and contacting the water-phase with a TMAE resin,
  • S/D solvent/detergent
  • step c) addition of at least one chelating agent to obtain a chelating agent concentration for example of 3 mM to 100 mM in the resulting water phase of step c),
  • step d precipitation of fibrinogen from the chelating agent containing water phase from step d), by adding glycine until a final concentration of about
  • step f) loading the filtered solution of step f) onto an anion exchange resin comprising trimethyl-amino groups grafted to a hydroxylated methacrylic polymer backbone via linking groups and washing off loosely bound substances with a wash buffer of about 12.0 mS/cm conductivity,
  • Subject matter of the present invention is also a fibrinogen enriched fraction obtainable according to the manufacturing process of the invention.
  • the fibrinogen concentrate is filled into final containers after sterile filtration and it may be stored in liquid, liquid frozen or lyophilised form.
  • Suitable containers are glass vials or bottles or plastic bags eventually comprising a membrane allowing lyophilisation while the bag is tightly sealed off for fluids.
  • Fibrinogen produced according to this process is characterised by very low amounts of impurities which ascertain the nativity of the product and allows long term treatment of people in need.
  • FXIII is preferable at the concentration contained, because it supports stabilisation of the formed fibrin, while an overload of this transglutaminase is avoided .
  • the term “comprising”, “comprise” or “comprises” can also be replaced by “consisting”, “consist” or “consists” without altering the disclosure of the description.
  • cryoprecipitate is a preferred source and in the following the cryo- precipitate serves as a typical source of fibrinogen in the further description of the manufacturing process of the invention.
  • cryoprecipitate is reconstituted or solubilised under suitable buffer conditions in particular at about neutral pH (6.9-7.0 for example in a solution buffer containing Na-citrate and NaCI), subjected to adsorption in particular with AI(OH) 3 and the resulting gel removed e. g. by centrifugation. The supernatant can then become virus inactivated for example by solvent/detergent (S/D) treatment.
  • S/D solvent/detergent
  • S/D compounds such as Triton (0-[4-(l, 1,3,3- Tetramethylbutyl) phenoxy]-polyethoxyethanole) and TnBP (Tri-n-butyl- phosphate) are in particular removed by extraction with castor oil.
  • TnBP Tri-n-butyl- phosphate
  • the water-phase can be subjected to a chromatographic process. Typically this can be performed by contacting the water-phase with a strong an- ion-exchange gel, tri-methyl-amino-ethyl (TMAE) grafted on matrix material, such as Fractogel ® EMD-TMAE.
  • TMAE tri-methyl-amino-ethyl
  • Suitable chelating agents are Ca 2+ -chelating agents in particular l,2-bis(o-amino)ethane- ⁇ , ⁇ , ⁇ ', ⁇ '-tetraacetic acid (BAPTA), diethylene-triamine-pentaacetic acid (DTPA), ethylenediamine-tetraacetic acid (EDTA), ethylene-glycol-tetraacetic acid (EGTA) and nitrilo-triacetic acid (NTA) at concentrations of 3 mM to 100 mM, in particular of 5 mM to 50mM, even more particular of 5 mM to 20 mM .
  • a suitable precipitating agent for example glycine
  • glycine glycine
  • the resulting solution can be stirred for 60-120 min to precipitate fibrinogen.
  • Precipitation can be performed in a tem- perature range of +4.1°C to +40°C, as long as cryoprecipitation is omitted, in particular in the range of +5°C to 37°C, more particular from 5.1°C to 30°C, even more particular at 10°-20°C.
  • the fibrinogen containing precipitate can then be separated by centrifugation and this intermediate fibrinogen paste might be stored at ⁇ -60°C, preferably at -100°C to -65°C, for at least 6 months, if the intermediate fibrinogen paste is not processed without delay, but a storage time of 1 day up to 6 months is preferred.
  • a single precipitation e.g . with glycine provides a fibrinogen paste sufficiently pure for further processing .
  • the suspension obtained can then be filtered off and subjected to ultra/diafiltration for example against 5 times of the suspension volume of the same or a different buffer.
  • the resulting fibrinogen containing solution is then loaded onto an anion- exchange gel preferably selected from a group of tertiary or quaternary amino groups as ligands grafted to a matrix.
  • Said functional groups are selected from well known diethyl-amino-ethyl (DEAE) or, in the case of a strong anion exchange gel, from groups such as tri-methyl-amino, tri-methyl-amino-ethyl (TMAE) and other groups whereas the carrier material may be composed of cellulose, agarose, silica, polymeric or ceramic material.
  • the effective reduction of the sticky fibronectin is very advantageous for optional filtrations, such as ultra/diafiltration or nanofiltra- tion, as the lifetime of filters is increased due to reduced clogging .
  • the chromatographic gel or resin is in particular preequilibrated with the same buffer as used for re- suspending the intermediate fibrinogen paste before applying the fibrinogen solution.
  • Fibrinogen can then be eluted from the chromatographic column with an elution buffer containing 1.5 g/l sodium citrate, and 10.0 g/l glycine in particular adjusted to the same pH range as the washing buffer e.g. by HCI and/or NaOH and adjusted with about 7.0 g/l NaCI to the conductivity of 13.1-15 mS/cm at room temperature of 20°C -25°C.
  • a filtration in particular a nanofiltration is performed .
  • This filtered fibrinogen solution can further be concentrated by ultra/diafiltration to about 20-26 g/l and sterile filtered with membranes of ⁇ 0.2 pm nominal pore size.
  • concentrations such as 1-19.9 g/l or 26.01-30 g/l or even higher are also achievable.
  • the fibrinogen concentrate of the present invention may also be formulated with additives like stabilisers known by the skilled person such as carbohydrates, e.g. sucrose, trehalose, amino acids, e.g . glycine, histidine, alanine, arginine and detergents, e.g . poly- oxyethylene-(20)-sorbitan-monooleate (TWEEN 80 ® ).
  • This sterile filtered bulk is stored at -60°C or lower, in particular at -65°C to -80°C, before being sterile filtered for a second time and filled into final containers and optionally freeze dried or directly filled into final containers and optionally freeze dried without a second sterile filtration. It is not necessary to add further buffers, stabilisers, protease inhibitors, like AT- III, heparin-cofactor-II and Cl-esterase-inhibitor, or other compounds, like coagulation factor XIII (F XIII). Coagulation factor XIII is present in the concentrate with activities of >0.05 IU per mg fibrinogen (Clauss method), in particular with activities of 0.05-0.30 IU/mg .
  • the fibrinogen concentrate of the present in- vention is further characterised by a low content of compounds of higher molecular weight than fibrinogen (HMW), determined as % of total area by size exclusion chromatography at 280 nm.
  • HMW molecular weight
  • the fibrinogen concentrate of the present invention contains less than 11% HMW, in particular 2-10% when the concentration of the chelating agent was at least 3 mmol/l.
  • the use of chelating agents at concentrations of at least 5 mmol/l reduced the HMW-content to 2-6%.
  • Some albumin may also be present in a concentration of about 16 ng per mg fibrinogen.
  • Antithrombin-III (AT-III) and proteolytic activity were not detectible, i.e.
  • the invention is further explained by the following non-limiting examples.
  • Example I Cryoprecipitate, produced from plasma by established methods, was reconstituted or solubilised at about neutral pH, subjected to adsorption with AI(OH) 3 and the resulting gel removed by centrifugation. The supernatant was then virus in- activated by solvent/detergent (S/D) treatment. S/D compounds, according to EP-Al-0 131 740 were extracted with vegetable oil and the water-phase was contacted with Fractogel ® EMD-TMAE. Chromatographic conditions (pH-value of 6.9-7.1 and an osmolality of 570-610 mosmol/l) were employed under which the fibrinogen did not bind to the gel and hence was found in the flow-through or supernatant.
  • the fibrinogen containing precipitate was then separated by centrifugation, yielding an intermediate fibrinogen paste.
  • the resulting fibrinogen containing solution was then loaded onto GigaCap Q- 650M ® and the chromatographic gel or resin was preequilibrated with the same Tris buffer as used for resuspension before applying the fibrinogen solution.
  • Loosely bound substances were washed out with the equilibration buffer followed by washing with a wash buffer (1.5 g /I sodium citrate, 6.0 g /I sodium chloride, adjusted to about pH 7.0 and a conductivity of about 12.0 mS/cm).
  • Fibrinogen was then eluted from the chromatographic column with an elution buffer (1.5 g/l sodium citrate, and 10.0 g/l glycine adjusted to the same pH as the washing buffer and adjusted with about 7.0 g/l NaCI to the conductivity of 13.1-15 mS/cm). Nanofiltration was performed by successive passage of fibrinogen solution over nanofilters of decreasing pore size from 75nm down to ⁇ 35nm.
  • an elution buffer 1.5 g/l sodium citrate, and 10.0 g/l glycine adjusted to the same pH as the washing buffer and adjusted with about 7.0 g/l NaCI to the conductivity of 13.1-15 mS/cm.
  • the resulting fibrinogen solution was concentrated, formulated and sterile filtered. This sterile filtered bulk was stored for 5 days at -80°C before being sterile filtered for a second time and filled into final containers. One part of final con- tainers was lyophilised while the other part was kept as a liquid formulation. No detectable amounts of chelating agents were observed in the lyophilised product or the liquid concentrate.
  • Example II-XII were performed in the same way as example I but comprised variation of type and concentration of chelating agents as well as variations of extraction time. While parameters like protein content, fibrinogen-antigen content or fibrinopeptide-A content were not significantly influenced by these variations when being normalised to lmg fibrinogen, it was observed that the content of compounds of higher molecular weight than fibrinogen (HMW), determined by size exclusion chromatography, exceeded 10% when the concentration of the complexing agent was less than 3 mmol/l.
  • Example XIII was prepared according to the process of WO-Al-2012/038410, i.e. without any chelating agent present during purification. The outcome of these variations is summarised in table 1.
  • a set of experiments was performed to determine a suitable extraction time range as a compromise between yield and purity of the extracted fibrinogen in- termediate.
  • the suitable extraction time range was determined to be between 10 to 120 minutes as less extraction time provided a very pure intermediate at the cost of fibrinogen yield, while at extraction times exceeding 120 minutes it was observed that some impurities began to redissolve without a significant gain in fibrinogen yield .
  • a difference between the present invention and WO-A1-2012/038410 is represented by the addition of a chelating agent prior to precipitation of fibrinogen by a suitable precipitation agent, like glycine, and replacement of the following resuspension step in WO-A1-2012/038410 by an extraction .
  • Said modification resulted in an unexpected increase of coagulation factor XIII activity in the final product of the present invention, i.e. up to 0.30 IU/mg fibrinogen (fibrinogen concentration 20-25 mg/ml ; determined by the Clauss method), as well as an increased yield .
  • Figure 1 depicts a SDS-Page at non-reducing conditions revealing less high molecular weight compounds in typical products produced according to the process of the present invention (Lanes 6- 11 also indicated as “+”) compared to the product of patent application WO-A1-2012/038410 (Lanes 2-5 also indicated as "-").
  • the protein band closest to 250 kD represents fibrinogen while those above the fibrinogen band are compounds of higher molecular weight.
  • the protein band at about 50 kD represents albumin .
  • Lane 1 displays the molecular weight markers.
  • Figure 2 depicts a SDS-Page at reducing conditions. Tested products are the same as in figure 1 and in the same order and they are consequently indicated in the same manner as in figure 1, i.e. for products prepared by a process according to the present invention, while "-" indicates products prepared by a process according to WO-A1-2012/038410.
  • the major bands at about 50-70 kD represent the ⁇ -, ⁇ - and ⁇ -chains of fibrinogen .
  • the protein band at about 100 kD represent the dimer of the fibrinogen ⁇ -chain .
  • the faint band at about 30kD is caused by fibrinogen fragments.
  • Lane 1 displays the molecular weight markers. Comparison with WO-A2-2009/155626

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Abstract

Cette invention concerne un procédé de purification de fibrinogène à partir d'une source contenant du fibrinogène par précipitation du fibrinogène par un agent de précipitation à partir d'une solution contenant du fibrinogène en présence d'un ou de plusieurs agents de chélation et l'élimination du surnageant d'une pâte de fibrinogène, ledit procédé étant caractérisé en ce que le fibrinogène est extrait de la pâte pour former une fraction liquide contenant le fibrinogène, et un résidu non dissous, qui est séparé du liquide.
PCT/EP2013/054983 2012-03-12 2013-03-12 Procédé de production amélioré de fibrinogène et fibrinogène ainsi produit WO2013135684A1 (fr)

Priority Applications (9)

Application Number Priority Date Filing Date Title
CN201380013042.2A CN104321340B (zh) 2012-03-13 2013-03-12 用于生产纤维蛋白原的改进工艺及其生产的纤维蛋白原
RU2014139974A RU2663792C2 (ru) 2012-03-13 2013-03-12 Способ очистки фибриногена, продукт фибриногена и средство для очистки или производства продукта фибриногена
US14/382,712 US10112972B2 (en) 2012-03-13 2013-03-12 Process for production of fibrinogen and fibrinogen produced thereby
EP13709190.6A EP2825555B1 (fr) 2012-03-13 2013-03-12 Procédé amélioré de production de fibrinogène et fibrinogène produit selon ledit procédé
AU2013231321A AU2013231321B2 (en) 2012-03-13 2013-03-12 Improved process for production of fibrinogen and fibrinogen produced thereby
MX2014010492A MX351340B (es) 2012-03-13 2013-03-12 Proceso mejorado para la produccion de fibrinogeno y fibrinogeno producido por este.
ES13709190.6T ES2642383T3 (es) 2012-03-13 2013-03-12 Procedimiento mejorado de producción de fibrinógeno y fibrinógeno producido por el mismo
IL234226A IL234226B (en) 2012-03-13 2014-08-21 Improved process for production of fibrinogen and fibrinogen produced thereby
US16/136,003 US11401300B2 (en) 2012-03-12 2018-09-19 Process for production of fibrinogen and fibrinogen produced thereby

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US201261610030P 2012-03-13 2012-03-13
US61/610,030 2012-03-13
EP12159276 2012-03-13
EP12159276.0 2012-03-13

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US14/382,712 A-371-Of-International US10112972B2 (en) 2012-03-13 2013-03-12 Process for production of fibrinogen and fibrinogen produced thereby
US16/136,003 Division US11401300B2 (en) 2012-03-12 2018-09-19 Process for production of fibrinogen and fibrinogen produced thereby

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EP (1) EP2825555B1 (fr)
CN (1) CN104321340B (fr)
AU (1) AU2013231321B2 (fr)
ES (1) ES2642383T3 (fr)
MX (1) MX351340B (fr)
RU (1) RU2663792C2 (fr)
WO (1) WO2013135684A1 (fr)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014085861A1 (fr) 2012-12-05 2014-06-12 Csl Limited Procédé de purification de protéines thérapeutiques
CN104231072A (zh) * 2014-10-09 2014-12-24 江西博雅生物制药股份有限公司 一种从冷沉淀提取凝血因子ⅷ的废料中提取人纤维蛋白原的制备工艺
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EP3404037A4 (fr) * 2016-01-12 2019-08-21 Green Cross Holdings Corporation Procédé de purification de fibrinogène
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CN113214384B (zh) * 2021-04-26 2023-10-10 泰州博莱得利生物科技有限公司 犬纤维蛋白原的制备方法及其产品

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US9371355B2 (en) 2010-09-20 2016-06-21 Octapharma Ag Process for production of fibrinogen
US9938318B2 (en) 2010-09-20 2018-04-10 Octapharma Ag Process for production of fibrinogen
US11401300B2 (en) 2012-03-12 2022-08-02 Octapharma Ag Process for production of fibrinogen and fibrinogen produced thereby
WO2014085861A1 (fr) 2012-12-05 2014-06-12 Csl Limited Procédé de purification de protéines thérapeutiques
US10188965B2 (en) 2012-12-05 2019-01-29 Csl Behring Gmbh Hydrophobic charge induction chromatographic depletion of a protein from a solution
EP3483173A1 (fr) 2012-12-05 2019-05-15 CSL Behring GmbH Procede de separation de fibrinogen, fviii et/ou vwf de proteases plasmatique par hcic
US11426680B2 (en) 2012-12-05 2022-08-30 Csl Behring Gmbh Hydrophobic charge induction chromatographic protein depleted solution
US9598461B2 (en) 2013-02-04 2017-03-21 Csl Behring Gmbh Method of purifying therapeutic proteins
CN104231072A (zh) * 2014-10-09 2014-12-24 江西博雅生物制药股份有限公司 一种从冷沉淀提取凝血因子ⅷ的废料中提取人纤维蛋白原的制备工艺
EP3404037A4 (fr) * 2016-01-12 2019-08-21 Green Cross Holdings Corporation Procédé de purification de fibrinogène
US10815293B2 (en) 2016-01-12 2020-10-27 Green Cross Holdings Corporation Method for purifying fibrinogen

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AU2013231321B2 (en) 2017-05-25
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MX351340B (es) 2017-10-11
US10112972B2 (en) 2018-10-30
ES2642383T3 (es) 2017-11-16
AU2013231321A1 (en) 2014-09-11
MX2014010492A (es) 2014-11-14
US20190016755A1 (en) 2019-01-17
CN104321340B (zh) 2018-11-09
EP2825555A1 (fr) 2015-01-21
US20150045539A1 (en) 2015-02-12
RU2663792C2 (ru) 2018-08-09
RU2014139974A (ru) 2016-05-10
US11401300B2 (en) 2022-08-02

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